Note : Les descriptions sont présentées dans la langue officielle dans laquelle elles ont été soumises.
CA 02661357 2009-09-04
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386-01 CA/PCT
Method for producing 3-(2,2,2-trimethylhydrazinium)propionate dihydrate
The invention relates to a process for the preparation of pharmaceutically
active compounds, namely to the pharmaceutically active substance 3-(2,2,2-
trimethylhydrazinium)propionate dihydrate, the known medicine Meldonium
(INN) of formula (1)
(CH3)3N+NHCH2CH2C00-.2H20 (1)
Meldonium is a cardiovascular medicine with average daily dose 1.0g.
Because this preparation is used as an over-the-counter drug, a need for an
inexpensive large scale manufacturing process is needed. Known processes for
the preparation of Meldonium are not convenient for large scale production.
Therefore the aim of this invention are improvements in the method for
manufacturing Meldonium known hitherto allowing lower production costs and
application for large scale manufacturing processes.
A number of processes for the preparation of compound of the formula
(1) is known. A common scheme is used hitherto to produce this compound:
starting with 1,1-dimethylhydrazine and esters of acrylic acid, 3-(2,2-
dimethylhydrazino)propionic acid esters are prepared, which are alkylated by
an
appropriate alkylating agent (methyl chloride, methyl bromide, methyl iodide,
dimethylsulphate etc.). The halide or methylsulphate of alkyl-3-(2,2,2-
trimethylhydrazinium)propionate thus obtained is subjected to hydrolysis and
deionisation. Known methods for the preparation of Meldonium differ by the
approach to hydrolysis and/or deionisation of the corresponding 3-(2,2,2-
trimethylhydrazinium)propionate salt.
Thus a method is known, according to which solution of halide or
methylsulphate of alkyl- 3-(2,2,2-trimethylhydrazinium)propionate is treated
with
a strongly basic ion exchange resin, exchanging acid anion for hydroxyl anion,
followed by spontaneous alkaline hydrolysis (USP. 4,481,218). The method has
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many disadvantages: strongly basic ion exchangers are unstable and undergo
decomposition and oxidation during processing; they withstand only a limited
number of regeneration cycles; large quantities of solvents, acids and bases
as
well as deionised water are needed to regenerate the resins; low ion exchange
capacity and therefore high production costs of compound (1) by this process
are typical. This process is not convenient for large scale production of
Meldonium.
Some of the disadvantages mentioned above are avoided if alky1-3-
(2,2,2-trimethylhydrazinium)propionate salt is deionised by electrodialysis.
This
process in production of Meldonium is applied in two different technical
solutions (SU 1262900, RU 1262900, LV 5046 and Vasilyev V.N., Omel'chenko
Y.N., Tkach I.N., Pugovic 0.V., Kalvins I.J. Electromembrane synthesis of 3-
(2,2,2-trimethylhydrazinium)propionate. Zhurnal Prikladnoj Khimii (Journal of
Applied Chemistry, Rus), 1992, issue.12, vol. 65, pp. 2823-2825).
The disadvantage of this process is a need for highly specialised
equipment with enhanced requirements to the corrosion resistance of
constructive materials used (platinum plated titanium electrodes, controlled
diameter pore membrane, mechanical and chemical stability of membrane
material, ceramic coated constructive elements of the electrodialysis
equipment). The main parameters of electrodialysis process have to be
experimentally adapted ¨ current, flow speed, concentration of solutions,
distances between electrodes, form of the camera etc. Because of membrane
pollution during the production process, the parameters initially set should
be
constantly changed. The membrane undergoes degradation during the process
as well and has to be replaced regularly. Therefore the maintenance costs of
such equipment are high and the scaling-up of the process is complicated.
Simultaneously with dialysis, electrolysis of water takes place and explosive
gases are produced that cause safety problems. Therefore producing
Meldonium using electrodialysis is also rather expensive.
An alternative process of Meldonium production is known, according to
which in the first step 1,1-dimethylhydrazine is condensed with acrylic acid
trinnethylsily1 ester and the resulting product is alkylated to halogenide of
3-
(2,2,2-trimethylhydrazinium)propionate trimethylsilyl ester (RU 95118258.04).
This approach is based on the well known fact that trimethylsilylesters of
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carboxylic acids undergo spontaneous hydrolysis in water even without alkaline
catalysis. The main disadvantage of this process is the considerably high
costs
of trimethylsilyl esters of acrylic acid compared with methyl acrylate.
A standard method of alkaline hydrolysis of carbonic acid esters in case
of an alkyl-3-(2,2,2-trimethylhydrazinium)propionate salt could not be
successfully realised till now because of the problems of separation of 3-
(2,2,2-
trimethylhydrazinium)propionate dihydrate and the resulting inorganic salts.
It is
known that 3-(2,2,2-trimethylhydrazinium)propionate forms various double salts
(SU 849724, Lopyrev V.A., Dolgushin G.V., Voronkov M.G. Applied chemistry of
1,1-dimethylhydrazine and its derivatives. Zhumal Prikladnoj Khimii (Journal
of
Applied Chemistry, Rus), 1998, issue.8, vol. 71, pp. 1233-1248). Some of them
are very stable and can be used in agriculture as pesticides.
Our attempts to separate such double salts, for example double salt of
NaCI and 3-(2,2,2-trimethylhydrazinium)propionate, present in the crude 3-
(2,2,2-trimethylhydrazinium)propionate dihydrate obtained by hydrolysis of an
alkyl-3-(2,2,2-trimethylhydrazinium)propionate chloride by simple dissolving
or
heating the product in alcohol were unsuccessful. As a result some of NaCl
still
remained in the product as the double salt and all attempts to prepare pure 3-
(2,2,2-trimethylhydrazinium)propionate dihydrate (with content of the main
substance >99,5%) failed. We have prepared pure 3-(2,2,2-
trimethylhydrazinium)propionate double salt, for example, with Nal by treating
ethyl 3-(2,2,2-trimethylhydrazinium)propionate iodide with sodium ethylate and
established that it can be crystallized from ethanol without separation into
constituents. Due to high solubility of 3-(2,2,2-
trimethylhydrazinium)propionate
dihydrate in water, this solvent also can not be used for separation of the
inorganic salt constituent.
A summary of solubilities of inorganic double salts was recently
published (C.H.Yoder, J.P.Rowand, Application of the simple salt lattice
energy
approximation to the solubility of minerals. American Mineralogist, Volume 91,
pages 747-752, 2006). The solubilities of the double salts are similar to the
solubilities of the less soluble constituent salts or lie between the
solubilities of
the constituent salts. Therefore standard crystallization is not the method of
choice for separation of the double salt constituents. It is known that double
salts can be separated into their constituents by multiple fractional
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crystallizations at different temperatures. While such approach can be used
for
inorganic salts, it is not useful for medicines due to risk of decomposition
of the
labile organic component.
Surprisingly, we have now found that double salts of 3-(2,2,2-
trimethylhydrazinium)propionate with the inorganic salts formed in the
hydrolysis process can be completely separated, if the reaction solution in
alcohol during precipitation of inorganic salts had been saturated with
gaseous
acid anhydride, namely carbon dioxide or sulphur dioxide. For example, the
double salt of 3-(2,2,2-trimethylhydrazinium)propionate with KBr can thus be
separated into its constituents and the inorganic salt can be completely
removed from 3-(2,2,2-trimethylhydrazinium)propionate by a simple filtration.
According to this approach 3-(2,2,2-trimethylhydrazinium)propionate dihydrate
can be prepared and purified to pharmaceutical grade (>99,5%) by using
conventional methods of purification (crystallisation).
The present process can be conveniently used for conversion of alky1-3-
(2,2,2-trimethylhydrazinium)propionate chloride, bromide or methyl sulphate,
as
well as other easily hydrolysable ester of 3-(2,2,2-
trimethylhydrazinium)propionate salt, for example ¨ benzy1-3-(2,2,2-
trimethylhydrazinium)propionate salt. The amounts of alkaline agent can be
used from equimolar ratio to more then double excess of the base, preferably
1.05-2.15 counted on 3-(2,2,2-trimethylhydrazinium)propionate ester salt.
This approach can be also used for conversion such intermediates as
halide or methyl sulphate of 3-(2,2,2-trirnethylhydrazinium)propionic acid. In
this
case esters of 3-(2,2,2-trimethylhydrazinium)propionate halide or methyl
sulphate can be hydrolized under acidic conditions with catalysis by HCI,
sulphuric acid, phosphoric acid etc., followed by neutralisation by an
appropriate
inorganic base (for example ¨ sodium, potassium, calcium or magnesium
hydroxide or another appropriate base, for example sodium, potassium, lithium
or caesium carbonate or bicarbonate etc.) and the double salts thus obtained
can be easily separated by the invented process using saturation of the
solution
with carbon dioxide or sulphur dioxide.
The invented method for producing 3-(2,2,2-
trimethylhydrazinium)propionate dihydrate provides for the object of this
invention ¨ to develop a convenient and inexpensive large scale manufacturing
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process of the target compound, which differs from known processes by the
separation of 3-(2,2,2-trimethylhydrazinium)propionate double salts using
carbon dioxide or sulphur dioxide, which has a number of advantages over the
known processes. Thus, the novel method involves use of inexpensive and
available reagents (sodium, potassium hydroxide or another appropriate base,
carbon dioxide or sulphur dioxide, ethanol or propano1-2), easily available
and
common chemical technology equipment (reactors, vessels for crystallisation,
centrifuges etc.). Said process is fast and gives high yields of high purity 3-
(2,2,2-trimethylhydrazinium)propionate dihydrate or Meldonium (>99.5%) after
simple crystallisation. Therefore the invented process enables to
inexpensively
produce high quality Meldonium.
Examples
The ethanol used in the following examples, if not mentioned otherwise,
was commercial ethanol, containing approximately 95% by volume of ethanol
and 5% of water.
Example 1
66.8 g of KOH (content of the main substance 90%) were suspended in
450 ml of ethanol and, at 18-20 C 120.5 g of methy1-3-(2,2,2-
trimethylhydrazinium)propionate bromide were added during 5-10 min under
stirring. The stirring was continued at 18-20 C until ester saponification
was
complete (controlled by TLC). The mixture was then cooled to 2-4 C, and
saturated with CO2 to pH 8.1-8.5. The precipitate thus formed was filtered
off,
washed with 3x20 ml of ethanol and the combined filtrates were evaporated.
89 g (92%) of semi-crystalline solid was obtained
(3-(2,2,2-
trimethylhydrazinium)propionate content 94%). Crystallization from ethanol or
propano1-2 or another appropriate solvent gave 3-(2,2,2-
trimethylhydrazinium)propionate dihydrate with m.p. 85-87 C (purity >99.5%).
Example 2
34.0 g of KOH (content of the main substance 90%) were suspended in
450 ml of ethanol and at 18-20 C, 120.5 g of methyl-3-(2,2,2-
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trimethylhydrazinium)propionate bromide during 5-10 min were added under
stirring. The stirring was continued at 18-20 C until ester saponification
was
complete (controlled by TLC). The mixture was then cooled to 2-4 C, and
saturated with CO2 to pH 8.1-8.5. The precipitate thus formed was filtered
off,
washed with 3x20 ml of ethanol and combined filtrates were evaporated. 90 g
(93%) of semi-crystalline solid were obtained (3-
(2,2,2-
trimethylhydrazinium)propionate content 93%. Crystallization from ethanol or
propano1-2 or another appropriate solvent gave 3-
(2,2,2-
trimethylhydrazinium)propionate dihydrate with m.p. 85-87 C (purity >99.5%).
Example 3
66 g of KOH (content of the main substance 90%) were suspended in
450 ml of ethanol and, at 18-20 C, 136 g
of methy1-3-(2,2,2-
trimethylhydrazinium)propionate methylsulphate were added under stirring
during 5-10 min. The stirring was continued at 18-20 C until the ester
saponification was complete (controlled by TLC). The mixture was then cooled
to 2-4 C, saturated with CO2 to pH 8.1 ¨ 8.5. Precipitate thus formed was
filtered off, washed with 3x10 ml of ethanol and the combined filtrates were
evaporated. 89.5 g (89%) of semi-crystalline solid was obtained.
Crystallization
from ethanol or propano1-2 or another appropriate solvent gave 3-(2,2,2-
trimethylhydrazinium)propionate dihydrate with m.p. 85-87 C (purity >99.5%).
Example 4
66 g of KOH (content of the main substance 90%) are suspended in
450 ml of ethanol and, at 18-20 C, 136 g
of methy1-3-(2,2,2-
trimethylhydrazinium)propionate methylsulphate were added under stirring
during 5-10 min. The stirring was continued at 18-20 C until the ester
saponification was complete (controlled by TLC). The mixture was then cooled
to 2-4 C, precipitate thus formed was filtered off and washed with 2x20 ml of
ethanol. Filtrates were combined and saturated with CO2 to pH 8.1-8.5.
Precipitate thus formed was filtered off, washed with 3x10 ml of ethanol and
the
combined filtrates were evaporated. 89.5 g (89%) of semi-crystalline solid
were
obtained (3-(2,2,2-trimethylhydrazinium)propionate content 91%) and finally
purified by electrodialysis. After evaporation the solid was crystallized from
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ethanol or propano1-2 or another appropriate solvent and gave 3-(2,2,2-
trimethylhydrazinium)propionate dihydrate with m.p. 85-87 C (purity >99.5%).
Example 5
24 g of NaOH were suspended in 450 ml of ethanol and, at 18-20 C,
136 g of methyl-3-(2,2,2-trimethylhydrazinium)propionate chloride during 5-10
min were added under stirring. The stirring was continued at 18-20 C until
ester
saponification was completed (controlled by TLC). The mixture was then cooled
to 2-4 C and saturated with CO2 to pH 8.1-8.5. Precipitate thus formed was
filtered off, washed with 3x10 ml of ethanol and the combined filtrates were
evaporated. 91 g (95%) of semi-crystalline solid were obtained (3-(2,2,2-
trimethylhydrazinium)propionate content 95%). Crystallization from ethanol or
propano1-2 or another appropriate solvent gave 3-
(2,2,2-
trimethylhydrazinium)propionate dihydrate with m.p. 85-87 C (purity >99.5%).
Example 6
33 g of NaOH were suspended in 450 ml of ethanol and, at 18-20 C,
92 g of methyl-3-(2,2,2-trimethylhydrazinium)propionate chloride during 5-
min were added under stirring. The stirring was continued at18-20 C until
ester saponification was completed (controlled by TLC). The mixture was then
cooled to 2- 4 C and saturated with CO2 to pH 8.1-8.5. Precipitate thus
formed
was filtered off, washed with 3x10 ml of ethanol and the combined filtrates
were
evaporated. 95 g (95%) of semi-crystalline solid were obtained (3-(2,2,2-
trimethylhydrazinium)propionate content 95%). During crystallization from
propano1-2 strongly basic ion exchange resin Amberlite IRA-400 is added in
amount corresponding to 1.2 equivalents of Cl- remaining, after 5 min the
resin
is filtered off, washed with 20 ml of ethanol and the combined filtrates
cooled. 3-
(2,2,2-trimethylhydrazinium)propionate dihydrate with m.p. 85-87 C. (purity
>99.5%) is obtained.
Example 7
33 g of KOH (content of the main substance 90%) are suspended in
450 ml ethanol and, at 18-20 C, 113.5 g of
methyl-3-(2,2,2-
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trimethylhydrazinium)propionate bromide were added under stirring during 5-10
min. The stirring was continued at 18-20 C until ester saponification was
complete (controlled by TLC). The mixture was then cooled to 2-4 C, inorganic
precipitate thus formed was filtered off and washed with 2x20 ml of ethanol.
Filtrates were combined and saturated with SO2 to pH 8.1-8.5. Precipitate
formed was filtered off, washed with 3x10 ml of ethanol and the combined
filtrates were evaporated. 90 g (93%) of semi-crystalline solid were obtained
(3-
(2,2,2-trimethylhydrazinium)propionate content 94%) and finally purified by
electrodialysis. The solid obtained after evaporation was crystallized from
ethanol or propano1-2 or another appropriate solvent and gave 3-(2,2,2-
trimethylhydrazinium)propionate dihydrate with m.p. 85-87 C (purity >99.5%).
Example 8
66 g of KOH (content of main substance 90%) were suspended in 450 ml
of ethanol and, at 18-20 C, 136 g of
methy1-3-(2,2,2-
trimethylhydrazinium)propionate bromide were added under stirring during 5-
min. The stirring was continued at 18-20 C until ester saponification was
completed (controlled by TLC). The mixture was then cooled to 2- 4 C.,
inorganic precipitate thus formed was filtered off and washed with 2x20 ml of
ethanol. Filtrates were combined and saturated with SO2 to pH 8.1-8.5.
Precipitate thus formed is filtered off, washed with 3x10 ml ethanol and the
combined filtrates were evaporated. 89 g (92%) of semi-crystalline solid were
obtained (3-(2,2,2-trimethylhydrazinium)propionate content 94%).
Crystallization
from ethanol or propano1-2 or another appropriate solvent gave 3-(2,2,2-
trimethylhydrazinium)propionate dihydrate with m.p. 85-87 C (purity >99.5%).
Example 9
Ethyl 3-(2,2,2-trimethylhydraziniumpropionate iodide was refluxed with 2
equivalents of sodium ethylate in absolute ethanol for 20 hours, cooled, the
precipitate filtered off, extracted with boiling methanol, the solution
evaporated
and the residue crystallized from absolute ethanol. Colourless crystals of the
double salt of 3-(2,2,2-trimethylhydrazinium)propionate and sodium iodide were
obtained, m.p. 186-188 C.
